EP3405653B1 - Procédé et dispositif pour réduire des pertes de fuite dans une turbine - Google Patents

Procédé et dispositif pour réduire des pertes de fuite dans une turbine Download PDF

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Publication number
EP3405653B1
EP3405653B1 EP17704540.8A EP17704540A EP3405653B1 EP 3405653 B1 EP3405653 B1 EP 3405653B1 EP 17704540 A EP17704540 A EP 17704540A EP 3405653 B1 EP3405653 B1 EP 3405653B1
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EP
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Prior art keywords
turbine
flow rate
working fluid
fluid
labyrinth seal
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EP17704540.8A
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German (de)
English (en)
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EP3405653A1 (fr
Inventor
Mario Gaia
Roberto Bini
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Turboden SpA
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Turboden SpA
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
    • F01D11/02—Preventing or minimising internal leakage of working-fluid, e.g. between stages by non-contact sealings, e.g. of labyrinth type
    • F01D11/04—Preventing or minimising internal leakage of working-fluid, e.g. between stages by non-contact sealings, e.g. of labyrinth type using sealing fluid, e.g. steam
    • F01D11/06—Control thereof
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
    • F01D11/001—Preventing or minimising internal leakage of working-fluid, e.g. between stages for sealing space between stator blade and rotor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
    • F01D11/02—Preventing or minimising internal leakage of working-fluid, e.g. between stages by non-contact sealings, e.g. of labyrinth type
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
    • F01D11/02—Preventing or minimising internal leakage of working-fluid, e.g. between stages by non-contact sealings, e.g. of labyrinth type
    • F01D11/04—Preventing or minimising internal leakage of working-fluid, e.g. between stages by non-contact sealings, e.g. of labyrinth type using sealing fluid, e.g. steam
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
    • F01D11/08—Preventing or minimising internal leakage of working-fluid, e.g. between stages for sealing space between rotor blade tips and stator
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
    • F01D11/08—Preventing or minimising internal leakage of working-fluid, e.g. between stages for sealing space between rotor blade tips and stator
    • F01D11/10—Preventing or minimising internal leakage of working-fluid, e.g. between stages for sealing space between rotor blade tips and stator using sealing fluid, e.g. steam
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2240/00—Components
    • F05D2240/55—Seals
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2260/00—Function
    • F05D2260/20—Heat transfer, e.g. cooling
    • F05D2260/232—Heat transfer, e.g. cooling characterized by the cooling medium
    • F05D2260/2322—Heat transfer, e.g. cooling characterized by the cooling medium steam

Definitions

  • the present invention relates to a method and a device suitable to reduce the losses due to leakage of fluid in a turbine.
  • the turbine is used for the expansion phase of vapor in thermodynamic cycles and is particularly suitable for an organic Rankine cycle (in the following, also an ORC cycle).
  • thermodynamic cycle As known, a finite sequence of thermodynamic (for example isothermal, isochoric, isobaric and adiabatic) transformations, is defined as a thermodynamic cycle, at the end of which the system returns to its initial state.
  • an ideal Rankine cycle is a thermodynamic cycle comprising two adiabatic transformation and two isobars, with two phase changes, from liquid to vapor and from vapor to liquid. Its purpose is to transform heat into work.
  • Such cycle is generally adopted principally in thermal power plants for the production of electrical power and uses water as working fluid, both in liquid and vapor form, with the so-called steam turbine.
  • ORC organic Rankine cycles
  • the plant for an ORC cycle includes one or more pumps for supplying the organic working fluid, one or more heat exchangers to realizing the preheating, vaporization and possible overheating or heating stages in supercritical conditions of the same working fluid, a vapor turbine for the expansion of the fluid, mechanically connected to an electric generator or a working machine, a condenser which returns the organic fluid in the liquid state and possibly a recuperator for recovering the heat downstream of the turbine and upstream of the condenser.
  • Labyrinth seals are an effective tool, but can not cancel the leakages.
  • the amount of fluid leakage depends on many factors (in particular on the involved pressures).
  • Such leakage can correspond in some cases to 10% of the power produced by the turbine and is mainly localized in the first one or ones stages of the machines, where the pressures are higher and the blade heights are smaller: in fact, the same gap is more or less significant depending on the blade heights, as it has a different percentage weight.
  • Figure 1 is a detail of the high pressure stages of a axial turbine 1 according to the known art. As will be discussed below, however what will be explained later can be extended to any type of axial, radial (centripetal or centrifugal) or mixed radial/axial turbine.
  • Figure 2 shows a detail of the first stage, still according to the known art.
  • the vapor of the organic working fluid enters the turbine with the evaporation pressure P1.
  • the vapor is accelerated in the first stator S1 and is guided towards the rotor blades R1, where it generates mechanical power.
  • the vapor pressure decreases from one stage to the other, until reaching at the exit of the turbine, a pressure value near to the condensation pressure.
  • the relationship between the inlet pressure P1 in the stator S1 and outlet pressure PI1 from the same first stator stage can also be greater than 2, i.e. the stator works as a nozzle with a sonic block.
  • the power associated to the decrease of the static pressure is converted in a dynamic pressure, i.e. in speed. In other words, between the upstream and downstream side of the stator, under adiabatic and isentropic conditions the total pressure (the sum of static and dynamic pressure) is preserved.
  • the accelerated vapor rate flow from the stator S1 will preferably move towards the rotor R1, but a portion of the same will directly flow downstream of the rotor R1 by passing through the labyrinths L2 placed at the top of the blades and a portion (corresponding to the flow rate Q traf) will instead flow through the labyrinths L1 placed closer to the axis of rotation.
  • Aim of the present invention is to devise a method permitting to minimize the energy content of leakage losses of the organic fluid passes through the stages of an ORC turbine and, consequently, to increase the efficiency of the turbine of a few percentage points.
  • the method according to the present invention uses a fluid injection in a vapor or liquid phase or in the form of a two-phase fluid and has the features referred to in the independent method claim 1.
  • the injected fluid may preferably be the same organic working fluid drawn from the same plant.
  • the concept of the present invention as will be seen below, can however be extended to any fluid.
  • Another aim of the present invention is to provide a device suitable to implement the above method by allowing to realize the fluid injection within the ORC turbine in the most advantageous areas.
  • the device according to the present invention is integrated in the ORC expansion turbine having the characteristics set out in the independent product claim.
  • a further aim of the present invention is to configure the ORC cycle system so that it is suitable to generate a flow rate of a working fluid, which is vaporized or is still in the liquid phase and can be injected into the turbine. This is done by providing the plant with an additional heat exchanger, as set out in the annexed claim 17.
  • a plant for ORC cycles comprises at least a supply pump 4 for supplying an organic working fluid, in a liquid phase, to at least one heat exchanger 5.
  • the organic liquid is heated until its transformation in the vapor phase and until its eventual overheating or it is hypercritically heated in case of a supercritical cycle.
  • the heat is supplied by a hot source, for example a diathermic oil.
  • the vapor passes through an expansion turbine 10 which produces the useful work of the cycle, i.e. the production of mechanical energy.
  • the working fluid finally passes through a condenser 3 which brings it in the liquid phase in order to be supplied again by the pump 4 to the heat exchanger.
  • a recuperator 2 can be inserted, i.e. a heat exchanger which exchanges heat between the organic fluid in liquid phase which is pumped by the pump 4 towards the heat exchanger 5, and the organic fluid in a vapor phase which from the turbine 10 is directed toward the condenser 3.
  • Figure 4 shows a detail of the first high pressure stage of the turbine 10, according to one aspect of the present invention.
  • the turbine 10 then includes a first row of stators S1 and a first row of rotors R1.
  • the blades of the stator stage S1 are integral with the housing 20 of the turbine, while the blades of the rotor stage R1 are integral with a disc 30 of the turbine.
  • the same turbine 10 also may include further rows of stators and row of rotors and can also be an axial, radial (centripetal or centrifugal) or a mixed radial/axial turbine.
  • the description of the method and of the device according to the invention will be referred purely by way of example to the first high pressure stage, as in Fig. 4 , as this is the stage in which the fluid pressure is highest and therefore the losses due to leakage are more considerable in terms of loss of turbine efficiency.
  • the first turbine stage can also be implemented in one or more successive stages, also in correspondence of the labyrinths placed between the turbine case and the top of the rotor blades.
  • the organic fluid at the turbine inlet, and hence upstream of the stator S1 stage has a total pressure P1, downstream of the same stator stage (i.e. upstream of the first rotor stage R1), will have a lower static pressure PI1, whereas downstream of the first rotor stage R1, the fluid will have a further pressure reduction and the value of the static pressure is be equal to P2, then consequently P2 ⁇ PI1 ⁇ P1.
  • the amount of the pressure reductions depends on the reaction of the turbine stage considered.
  • a labyrinth L11 is further considered, being identical to the L1 labyrinth (Figg. 3 and 4), located upstream of L1.
  • the volume between the two labyrinths will produce to a P int0LD pressure, which is intermediate between PI1 and Peon and is such that the flow rate of fluid leaking into the labyrinth between the PI1 and P int0LD pressures is equal to that leaking between the P int0LD and Pcond.
  • a volume I is supplied between the two labyrinths with a fluid flow rate Q.
  • the same working organic fluid could be used, the flow rate of which can be tapped, according to known methods and therefore it will be not described.
  • the injection of fluid can take place by means of a duct 21 passing within the housing 20 of the turbine.
  • the volume I into which the fluid is injected will be at a static pressure lower than the total pressure P1 upstream of the turbine.
  • the labyrinth L1 will be traversed by a vapor flow rate Q traf in practice identical to that which crossed it in the absence of the labyrinth L11, since the pressure difference upstream and downstream of L1 is the same as the case without injection ( Fig. 2 ); also in this case the maze L11 will not be affected by any pressure difference and thus will not be crossed by any vapor flow.
  • the flow rate may not be exactly identical to Q traf if the characteristics of the injected (superheated) vapor were not identical to those present in the same room in the absence of injection. However, this does not alter in any case the meaning and the scope of the present invention.
  • the labyrinth L11 is subjected to a zero pressure difference P I1 - P intNEW or otherwise a limited one, therefore L11 can be achieved with a less complex geometry with respect to L1.
  • the injection can take place directly within the labyrinth L1, through a conduit 22 which also passes through the housing 20 of the turbine, without the addition of a second group of labyrinths. Also, the injection can occur upstream of the single labyrinth L1.
  • FIG. 6 it is shown the temperature-power diagram ( Fig. 6a ) and the temperature-entropy (6b) of a typical ORC cycle.
  • the organic fluid receives heat from the high temperature source SC that consequently will lower its temperature, accomplishing the transformation thermodynamics from 01 to 02.
  • the SC source releases heat to the organic fluid in BC (pre-heating), CD (evaporation) and D-E (overheating) .
  • the hot source can be diathermal oil or directly geothermal fluid or the combustion or recovery gases of water vapor.
  • the turbine expands the fluid in EF, while the heat released in FG is transferred to AB (heat recovery), if a recuperator is present in the cycle.
  • the further heat possessed by organic fluid is then transferred to a cold source SF (condensation).
  • the injection of the organic working fluid in the labyrinths can be made according to three different modes, all selected so as to obtain the desired improvement in performance of the turbine:
  • the first mode provides an injection into the vapor labyrinth to a next pressure PI1, i.e. the pressure downstream of the first stator; the vapor at this intermediate pressure is generally not available and must be specially generated.
  • a solution is to draw off the organic fluid still in the liquid phase, for example at the outlet of regeneration B, laminate it and allow it to evaporate at a lower pressure in an additional heat exchanger (6 in Figure 8a ), by exploiting in the most convenient way the hot source SC.
  • the vapor production to an intermediate pressure level involves the absorption of a considerable power, but still at a lower temperature compared to the upstream vapor turbine conditions with a pressure P1.
  • the vapor upstream of the labyrinth L1 is in both cases (with and without injection) near to the static pressure PI1, but in the case without injection it is located at a higher total enthalpy level, almost equal to that in the turbine inlet.
  • the vapor used to "seal" the labyrinth has an energy content (total enthalpy) lower than that of the vapor that leaks normally from the labyrinth.
  • the power produced for the vapor at the turbine inlet conditions point E in FIG.
  • Fig. 7 is still a thermodynamic temperature-entropy diagram in which in addition to ORC cycle already illustrated in FIG. 6b are different possible choices of the lamination pressure are shown, at which to generate the vapor to be injected.
  • the choice of the lamination pressure P intNEW with respect to PI1, or if equal to PI1 or slightly higher or slightly lower is conditioned by the balancing of several factors:
  • the level of laminating pressure in fact determines the overall efficiency of the plant.
  • the liquid is evaporated at a sufficiently low temperature, it is possible to further lower the temperature of the hot source (from 02 to 03), and then recover more heat, as described in Figures 8a and 8b .
  • the low pressure vapor generation can be realized by an additional heat exchanger 6, fed downstream of the main heat exchanger 5.
  • a certain flow rate Q1 of oil can be separated from the main circuit to a suitable intermediate temperature (in the example below about 200°C) and with it in parallel with the additional heat exchanger 6.
  • Table 1 shows the performance increase that can be achieved thanks to the subject of the patent system in a typical case of ORC application.
  • the standard case (without application of the present invention, that is, according to the known art) refers to a plant of cyclopenthane, as represented in Figure 6 .
  • the other two cases instead refer to the same plant in which the injection system has been implemented in the labyrinths, respectively according to the diagrams of Figures 8 and 9 .
  • the vapor turbine inlet conditions are 25 bar and 250°C, while the pressure PI1 in this example is equal to 12 bar; the hot spring is diathermic oil to 315° C.
  • Tabella 1 Property Standard Injection ( Fig. 8 ) Injection ( Fig.
  • the second mode of generation of vapor at lower pressure provides that the organic liquid is withdrawn in liquid form in the most convenient point in the system and injected into the labyrinth, where it tends to evaporate because it absorbs heat from the hot walls of the turbine, but especially by the vapor already present in the chamber: the liquid impacting against the rotating surfaces tends to be distributed in form of drops that increase the thermal exchange surface with the surrounding vapor.
  • the evaporating fluid increases its volume and the pressure inside the chamber, limiting the leakage.
  • the advantage compared to the previous mode is that it uses fluid in the liquid state and not vapor, hence with a lower energy content.
  • the disadvantage may be represented by the tensional stress that may be created in the material forming the stator and rotor components in localizing lowering of temperature due to the introduction of cold liquid.
  • the organic fluid may leak out of the labyrinth still in the liquid state, segregating in certain areas of the turbine or impacting on downstream blades.
  • the third mode of the vapor generation instead takes its cue from what has just been described as a possible disadvantage of the previous mode: the liquid is injected in the chamber delimited by the labyrinth, so as to spread, in form of droplets; part of the fluid evaporate, while another part remains in a liquid form. This mixture of vapor and drops will tend to flow more laboriously through the labyrinths games, limiting the leakage.
  • the labyrinth L1 is typically affected by a difference pressure highly above the critical pressure ratio, then the vapor that leaks will have a sonic speed equal to that in the vicinity of the minimum passage section. If to the vapor liquid droplets are united, these obstruct the passage of vapor in the vicinity of the throat, reducing the passage area for the vapor.
  • the invention relates to systems that operate according to an organic Rankine cycle (ORC) in particular to the case where the expansion ratio around the object considered is at least 1.5, in a manner that the energetic content of the vapor injected to the labyrinth becomes significantly lower than that of the main flow in correspondence of that stage.
  • ORC organic Rankine cycle

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Turbine Rotor Nozzle Sealing (AREA)

Claims (20)

  1. Procédé pour réduire les pertes d'un fluide organique de travail à l'intérieur d'une turbine (10) d'un système à cycle organique de Rankine, le procédé comprenant l'injection d'un débit de fluide (Q) dans un volume (l) avec une pression statique inférieure à la pression totale (P1) en amont d'un étage dans lequel l'injection est réalisée et située à proximité d'au moins un joint de labyrinthe (L1, L11) d'au moins un étage de turbine (10), ledit débit de fluide (Q) ayant une teneur éxergétique initiale inférieure à la teneur éxergétique initiale du fluide organique de travail situé à l'intérieur de la turbine et traversant ledit joint à labyrinthe (L1, L11).
  2. Procédé selon la revendication 1, dans lequel le volume (1) est disposé à proximité du premier étage de la turbine (10).
  3. Procédé selon la revendication 1, dans lequel le volume dans lequel l'injection du débit de fluide (Q) est réalisée est disposé dans une position proche d'un étage de turbine (10), différent du premier étage et est à une pression statique inférieure à la pression totale en amont de l'étage de turbine correspondant dans lequel a lieu l'injection.
  4. Procédé selon l'une des revendications précédentes, dans lequel le débit de fluide (Q) est injecté précisément dans un premier joint de labyrinthe (L1).
  5. Procédé selon l'une des revendications 1 à 3, dans lequel le débit de fluide (Q) est injecté en amont du premier joint de labyrinthe (L1).
  6. Procédé selon l'une des revendications 1 à 3, dans lequel le débit de fluide (Q) est injecté à l'intérieur du volume (1) en amont du premier joint de labyrinthe (L1) et en aval d'un deuxième joint de labyrinthe (L11).
  7. Procédé selon l'une des revendications 1 à 6, dans lequel le débit (Q) du fluide organique de travail est injecté en phase vapeur.
  8. Procédé selon l'une des revendications 1 à 6, dans lequel le débit (Q) du fluide organique de travail est injecté dans une phase liquide.
  9. Procédé selon la revendication 8, dans lequel le débit (Q) du fluide organique de travail se vaporise à proximité dudit au moins un joint de labyrinthe (L1, L11).
  10. Procédé selon la revendication 8, dans lequel le débit (Q) du fluide organique de travail est transformé en un mélange en deux phases proche dudit au moins un joint de labyrinthe (L1, L11).
  11. Procédé selon au moins l'une des revendications 1 à 10, dans lequel le débit (Q) du fluide organique de travail est pris en aval d'un récupérateur (2) du système ORC.
  12. Procédé selon l'une des revendications 7 et 11, dans lequel le débit (Q) du fluide organique de travail est pris en phase liquide en aval du récupérateur (2), puis il est laminé et enfin vaporisé dans un échangeur de chaleur (6) supplémentaire.
  13. Turbine d'expansion ORC (10) comprenant:
    - un boîtier (20) de turbine connecté de manière stable avec au moins un premier étage de stator (S1) ;
    - au moins un disque (30) connecté en permanence à au moins un premier étage de rotor (R1);
    - au moins un joint de labyrinthe (L1, L11) disposé en aval dudit au moins premier étage de stator;
    caractérisée par au moins un conduit (21, 22) traversant le boîtier (20) de la turbine qui relie de manière fluide l'extérieur de la turbine au volume interne de la turbine et est configuré pour injecter un débit (Q) d'un fluide à proximité d'au moins un joint de labyrinthe (L1, L11), ledit débit de fluide (Q) ayant une pression statique inférieure à la pression totale (P1) en amont d'un étage dans lequel l'injection a lieu, et un contenu exergétique initial est inférieur au contenu exergétique initial du fluide organique de travail disposé à l'intérieur de la turbine et traversant ledit joint de labyrinthe (L1, L11).
  14. Turbine d'expansion selon la revendication 13, caractérisée en ce que la turbine est configurée de telle sorte que le débit de fluide (Q) est injecté à travers un premier conduit (22) exactement à l'intérieur du premier joint de labyrinthe (L1).
  15. Turbine à expansion selon la revendication 13, caractérisée en ce que le débit de fluide (Q) est injecté à travers le premier conduit (22) en amont du premier joint de labyrinthe (L1).
  16. Turbine d'expansion selon la revendication 13, caractérisée en ce que le débit de fluide (Q) est injecté à travers un deuxième conduit (21) dans le volume (l) en amont du premier joint de labyrinthe (L1) et en aval d'un deuxième joint de labyrinthe (L11).
  17. Système de cycle organique de Rankine (ORC), comprenant:
    - un récupérateur (2) configuré pour transférer la chaleur d'un fluide organique de travail en phase vapeur au même fluide organique de travail en phase liquide;
    - un condenseur (3) en aval du récupérateur (2), configuré pour transférer la chaleur du fluide organique de travail en phase vapeur vers une source froide (SF);
    - des moyens de pompage (4) en aval du condenseur (3), configurés pour alimenter le fluide organique de travail en phase liquide vers un échangeur de chaleur (5) avec une pression prédéterminée (P1);
    - un échangeur de chaleur (5) configuré pour chauffer, vaporiser et éventuellement surchauffer le fluide organique de travail au moyen d'une source chaude (SC);
    - une turbine d'expansion (10) configurée pour détendre le fluide organique de travail en phase vapeur d'une pression (P1) à une pression inférieure (Pcond), le système ORC étant caractérisé en ce que ladite turbine (10) est configurée selon l'une des revendications 13 à 16.
  18. Système à cycle organique de Rankine selon la revendication 17, caractérisé par un échangeur de chaleur supplémentaire (6), en aval de l'échangeur de chaleur (5) et configuré pour vaporiser au moyen de la source chaude (SC) du débit (Q) du fluide organique de travail, pris en phase liquide en aval de la pompe (4) ou du récupérateur (2).
  19. Système à cycle organique de Rankine selon la revendication 18, caractérisé en ce que l'échangeur de chaleur supplémentaire (6) est traversé par une fraction du débit de la source chaude (SC).
  20. Système à cycle organique de Rankine selon la revendication 17, caractérisé en ce que l'échangeur de chaleur supplémentaire (6) est disposé en parallèle par rapport à au moins une partie de l'échangeur de chaleur (5) et est configuré pour vaporiser, par le débit (Q1) de la source chaude (SC), un débit (Q9) du fluide organique de travail, versée dans la phase liquide en aval de la pompe (4) ou du récupérateur (2).
EP17704540.8A 2016-01-20 2017-01-18 Procédé et dispositif pour réduire des pertes de fuite dans une turbine Active EP3405653B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ITUB2016A000240A ITUB20160240A1 (it) 2016-01-20 2016-01-20 Metodo e dispositivo per ridurre le perdite di trafilamento in una turbina
PCT/IB2017/050256 WO2017125858A1 (fr) 2016-01-20 2017-01-18 Procédé et dispositif pour réduire des pertes de fuite dans une turbine

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EP3405653A1 EP3405653A1 (fr) 2018-11-28
EP3405653B1 true EP3405653B1 (fr) 2020-02-05

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EP (1) EP3405653B1 (fr)
IT (1) ITUB20160240A1 (fr)
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US10895164B2 (en) 2021-01-19
US20190024524A1 (en) 2019-01-24
EP3405653A1 (fr) 2018-11-28
ITUB20160240A1 (it) 2017-07-20
WO2017125858A1 (fr) 2017-07-27

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